首页> 外文会议>International Conference on Environmental Science and Technology >INVESTIGATING EFFECTS OF GAS FLOW RATE AND CARBON DIOXIDE COMPOSITION IN CHEMICAL ABSORPTION OF CARBON DIOXIDE IN A PACKED BED USING SODIUM HYDROXIDE
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INVESTIGATING EFFECTS OF GAS FLOW RATE AND CARBON DIOXIDE COMPOSITION IN CHEMICAL ABSORPTION OF CARBON DIOXIDE IN A PACKED BED USING SODIUM HYDROXIDE

机译:使用氢氧化钠研究气体流速和二氧化碳组合物在填充床中二氧化碳化学吸收的影响

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In recent years, the removal of CO_2 from industrial gas streams has become mportant.This has resulted from the environmental concern for reduction of greenhouse as emissions from industrial sources. Here, CO_2 is considered to be the largest ontributor to the global warming problem, and is thus the major target for reduction. The emoval of CO_2 from gas streams can be achieved by absorption into a liquid solvent. his separation process usually takes place in the columns packed with packing aterials to promote direct contact between irrigating liquid and the continuous gas hase, in this study simulation of carbon dioxide absorption by Sodium Hydroxide olution in a packed bed has been investigated. first, mass and energy balances were applied around a differential height of the bed. So, the governing equations were obtained. These equations are related to both phases: gas phase and liquid phase. Gas phase consists of carbon dioxide and air which we just consider carbon dioxide in the equations. On the other hand liquid phase consists of sodium hydroxide, water and sodium carbonate. So we have a general differential equation for each phase and one equation for each substance in both phases. Surface renewal theory by Danckwerts was used to represent the mass transfer operation. The differential equations we obtained should be solved to represent the exit concentration of carbon dioxide in gas phase. Since half of the boundary conditions were not known we used shooting method to estimate these boundary conditions and fourth order runge-kutta method was used to solve the differential equations by MATLAB software. A verification of model was carried out by comparison with the experimental data taken from the packed bed. Gas samples were analyzed by gas chromatography. The predicted results and actual data represent an appreciable agreement.
机译:近年来,从工业气体流中取出CO_2已经变得普及。这导致了环境问题,将温室减少为工业来源的排放。这里,CO_2被认为是全球变暖问题的最大的作用,因此是减少的主要目标。通过吸收到液体溶剂中可以实现来自气流的CO_2。他的分离过程通常发生在填充有填充物体的柱中,以促进灌溉液和连续气体散列之间的直接接触,在本研究中研究了填充床中的氢氧化钠铝的二氧化碳吸收的模拟。首先,围绕床的差动高度施加质量和能量余量。因此,获得了管理方程。这些方程与两阶段有关:气相和液相。气相由二氧化碳和空气组成,我们只考虑等式中的二氧化碳。另一方面,液相由氢氧化钠,水和碳酸钠组成。因此,我们对两个阶段中的每个阶段的一般微分方程和每个物质的一个方程。 Danckwerts的表面更新理论用于表示传质运行。我们获得的微分方程应该被解决,以表示气相中二氧化碳的出口浓度。由于未知边界条件的一半,我们使用拍摄方法来估计这些边界条件和第四阶runge-Kutta方法用于解决Matlab软件的微分方程。通过与从填充床取出的实验数据进行比较来进行模型的验证。通过气相色谱分析气体样品。预测结果和实际数据表示可观的协议。

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